SYSTEM AND METHOD FOR COMPRESSING NATURAL GAS

Abstract: A system and method for refueling vehicle storage tanks (16) with compressed natural gas (CNG) are provided that utilize a single stage compressor (14) operable at suction pressures ranging from about 330 to about 3600 psig and discharge pressures ranging from about 330 to about 4500 psig.

Description: SYSTEM AND METHOD FOR COMPRESSING NATURAL GAS BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to natural gas refueling systems, and more particularly, to a system and method for compressing natural gas and for refueling motor vehicles. 2. Description of Related Art The use of compressed natural gas ("CNG") as an alternative fuel for motor vehicles is well known. Natural gas is in most cases a less costly and cleaner-burning fuel than gasoline. One disadvantage of natural gas as a motor vehicle fuel is the volume required to store the quantity of gas needed to provide a range of travel comparable to that experienced with gasoline. In order to store a sufficient volume of natural gas to provide a reasonable range of travel, it has been thought desirable to compress the natural gas to a pressure of about 3000 to 3600 psi or higher. Because the vehicle tank pressures needed to store sufficient natural gas to provide a reasonable range of travel are relatively high when compared to available consumer line pressures, the refueling of vehicle storage tanks presents yet another problem. Refilling vehicle storage tanks with CNG within a time period comparable to that required to refill conventional vehicle fuel tanks with gasoline can necessitate the use of large, expensive, multistage compressors. Alternatively, home or on-board CNG refueling systems have been developed that can deliver the compressed gas at the required pressure, but such systems are characterized by very low flow rates, necessitating long periods (such as overnight) for refueling. Among the various systems for refueling vehicle storage tanks that have previously been disclosed, one conventional system uses a large, multistage compressor to compress the natural gas to about 4000 psi or greater and then holds the CNG in large volume intermediate storage tanks at that pressure. During refueling, the CNG is allowed to flow into the vehicle storage tanks until the vehicle tank pressure is about 3000 psi. After refueling, the intermediate storage is replenished with sufficient gas to again raise the storage pressure to about 4000 psi. This system is inefficient because of the repetitive need to charge storage tanks to about 4000 psi. Another system, disclosed in U.S. 4,646,940, utilizes a differential pressure measuring apparatus in controlling CNG refueling. The patent discloses preferentially refueling the CNG tanks of a vehicle first from low pressure, then intermediate pressure, and finally, high pressure storage tanks. A reference cylinder at 2750 psi is used to cut off the refueling operation. U.S. 4,501,253 discloses a low volume (approximately one cubic foot per minute) on-board automotive methane compressor for refilling vehicle storage tanks by compressing the gas from available line pressure to about 2000 to 3000 psi. U.S. 4,515,516 and 5,169,295 disclose systems in which liquid pressure is used to boost CNG pressures in a storage/refueling process. U.S. 4,515,516 discloses a home use natural gas refueling system in which a liquid is used to boost the gas from line pressure to greater than 2000 psi. The system utilizes a variable rate pump which pumps the compression fluid at a high rate for low pressures and a low rate for high pressures. (An illustrative flow rate is about one gallon per minute of compression fluid above 600 psi.) U.S. 5,169,295 discloses a higher volume liquid-based compression system that can be mounted on a car, truck, boat, train or plane, but is preferably mounted on a tractor trailer truck with the hydraulic pumps connected to the tractor engine by a transfer case. The maximum pressure of the liquid supplied from the liquid supply means is less than the ' minimum pressure of the gas from the gas-supplying conduit. In the preferred embodiment the supply pump has an maximum output pressure of about 350 psig, and the maximum pressure of the gas-supplying conduit may range from about 400 to about 2900 psig. Illustrative pumping rates for the compression liquid range up to about 200 gpm. Other previously disclosed CNG refueling systems utilize adsorbent-filled cylinders to reduce the tank pressure needed to store a predetermined amount of natural gas. Such systems are disclosed, for example, in U.S. 4,522,159; 4,531,558; and 4,749,384. SUMMARY OF THE INVENTION According to the present invention, a CNG refueling system and method are provided that will enable motor vehicle storage tanks to be refueled quickly and efficiently through the use of a single stage compressor that is operable over a wide range of suction pressures in combination with means for temporarily storing the CNG at a preferred intermediate storage pressure of from about 1700 to about 2700 psig, and most preferably from about 2300 to about 2400 psig (based on a storage temperature of about 70° F) and means for selectively supplying gas to the compressor at the intermediate storage pressure. Because the most efficient storage pressure for natural gas at 70° F ranges from about 1700 to about 2700 psig, within this pressure range the greatest volume of gas can be withdrawn from storage with the smallest attendant reduction in storage vessel pressure. By selectively controlling the inlet gas supply to the compressor between an external (relatively low pressure) supply line and intermediate storage vessels, thereby taking advantage of the higher density of gas drawn from the intermediate storage vessels, one can achieve an increase in compressor capacity without increasing horsepower or energy consumption. Where the desired maximum vehicle tank pressure exceeds about 3000 psig, refueling rates can be increased and horsepower requirements reduced by first delivering CNG to the vehicle storage tanks simultaneously from the compressor and from the intermediate storage tanks until the vehicle tank pressure equalizes with the intermediate storage pressure, and then by "topping off the tanks with CNG supplied to the compressor from intermediate storage at pressures ranging between 1700 and 2700 psig. Whereas a 20 horsepower compressor may, for example, compress about 97 cfm natural gas from a suction pressure of about 800 psig to a discharge pressure of about 3000 psig, the same 20 horsepower compressor may compress about 345 cfm natural gas from a suction pressure of about 2500 psig to a discharge pressure of about 3000 psig. This increased CNG delivery rate at higher pressures enables a user to fill vehicle storage tanks quickly and efficiently to pressures greater than 3000 psig. According to one embodiment of the invention, a CNG vehicle refueling system is provided that comprises: Means for selectively delivering natural gas received from an external source directly to a motor vehicle storage tank at the available line pressure; means for simultaneously delivering part of the natural gas received from the external source directly to the motor vehicle storage tank and for compressing part of the natural gas received from the external source and delivering the CNG to intermediate storage at a pressure higher than the available line pressure; means for simultaneously delivering CNG to the vehicle storage tank from the compressor discharge and from intermediate storage; means for selectively delivering CNG from the intermediate storage to the suction side of the compressor for further compression; means for delivering the further- compressed natural gas into the motor vehicle storage tank; and means for selectively refilling the intermediate storage with natural gas compressed from available line pressure after the vehicle storage tank is filled. According to another preferred embodiment of the invention, the subject refueling system comprises a single stage compressor operable over a range of suction pressures extending, for example, from about 330 to about 3600 psig with a discharge pressure of up to about 4500 psig, in combination with means for temporarily storing the compressed gas in intermediate storage at a pressure ranging between about 330 and about 3600 psig (preferably between about 1700 and about 2700 psig, and most preferably between about 2300 and about 2400 psig), and means for selectively controlling the supply of gas to the suction side of the compressor from either a relatively low pressure source such as a natural gas transmission line or from the intermediate storage. According to another embodiment of the invention, a motor vehicle refueling system is provided that comprises in combination: A single stage compressor connectable to a source supplying natural gas at a pressure ranging from about 330 to about 1000 psig that is operable at suction pressures ranging from about 330 to about 3600 psig and at discharge pressures ranging from about 330 to about 4500 psig; intermediate storage means for temporarily storing CNG at intermediate storage pressures ranging from about 330 to about 3600 psig, preferably from about 1700 to about 2700 psig, and most preferably from about 2300 to about 2400 psig; means for supplying natural gas received from the external source directly to a motor vehicle storage means at a supply pressure ranging from about 330 to about 1000 psig; means for simultaneously supplying CNG to the vehicle storage means from the intermediate storage means and from the compressor until the pressure in the vehicle storage means equalizes with the intermediate storage pressure; means for further compressing CNG supplied from the intermediate storage means up to the maximum intended fill pressure for the vehicle storage means, preferably from about 3000 to as high as about 4500 psig, to complete filling the vehicle storage means; and means for compressing natural gas from the source pressure up to the desired intermediate storage pressure to refill the intermediate storage means after the refueling the vehicle storage means. According to another embodiment of the invention, a method for refilling vehicle storage tanks with CNG is provided that comprises the step of using CNG supplied from intermediate storage at a pressure ranging from about 330 to about 3600 psig, preferably from about 1700 to about 2700 psig, and most preferably from about 2300 to about 2400 psig, as the feed to a compressor that is capable of further pressurizing the CNG to a discharge pressure as high as the intended maximum fill pressure of the vehicle storage tanks, ranging up to about 4500 psig, and most preferably from about 3000 to about 3600 psig. By using CNG temporarily stored at a pressure ranging from about 1700 to about 2700 psig to supply a refueling compressor, one can "top off vehicle storage tanks quickly and more efficiently than has been achieved through the use of prior art methods. According to another embodiment of the invention, a method for refueling vehicle storage tanks with CNG is provided that comprises the steps of: Supplying natural gas at a pressure ranging from about 330 to about 1000 psig to a single stage compressor that is operable at suction pressures ranging from about 330 to about 3600 psig with attendant discharge pressures ranging from about 330 to about 4500 psig; compressing and temporarily storing CNG at intermediate storage pressures ranging from about 330 to about 3600 psig, preferably from about 1700 to about 2700 psig, and most preferably from about 2300 to about 2400 psig; compressing CNG from the supply pressure (about 330 to about 1000 psig) to the vehicle storage tank pressure and. discharging the CNG to the vehicle storage tanks while simultaneously supplying CNG to the vehicle storage tanks from the intermediate storage tanks and while allowing the vehicle storage tank pressure to equalize with the intermediate storage tank pressure; when the vehicle storage tank pressure has equalized with the intermediate storage tank pressure, supplying CNG to the compressor from the intermediate storage tanks and further compressing the CNG up to the intended full vehicle storage tank pressure, preferably from about 3000 to about 4500 psig, and most preferably from about 3000 to about 3600 psig, until the vehicle storage tanks are filled; and thereafter refilling the intermediate storage tanks with CNG supplied to the compressor at about 330 to about J000 psig until such time as the intermediate storage tanks are again filled to a predetermined pressure ranging from about 330 to about 3600 psig, preferably from about 1700 to about 2700 psig, and most preferably from about 2300 to about 2400 psig. According to one preferred embodiment of the method of the invention, when the vehicle storage tank pressure is below the available line pressure (preferably from about 330 to about 1000 psig) at which natural gas is supplied to the compressor suction at the start of refueling, the vehicle storage tank pressure is allowed to equalize with the available line pressure prior to supplying CNG to the vehicle storage tanks either from the compressor or from the intermediate storage tanks. While in this mode of operation, if the pressure in the intermediate storage tanks is below a predetermined desirable level such as, for example, preferably from about 1700 to about 2700 psig, and most preferably from about 2300 to about 2400 psig, the compressor can be used to refill the intermediate storage tanks to the predetermined desirable pressure level while the vehicle storage tank pressure is equalizing with the available line pressure. As used herein, the term "available line pressure" is used to include any source (other than the storage tanks of the vehicle being refueled) of natural gas at a pressure ranging from about 330 to about 1000 psig. Where the actual available line pressure is lower than about 330 psig, the use of a booster pump or other similarly satisfactory means may be required in order to raise the line pressure to a level of at least about 330 psig. BRIEF DESCRIPTION OF THE DRAWINGS The apparatus of the invention is further described and explained in relation to the following figures of the drawings wherein: FIG. 1 is a simplified block flow diagram depicting the CNG refueling system of the invention; and FIG. 2 is a graph showing compressor discharge rates plotted against suction pressures at a discharge pressure of 3600 psig for 20 and 40 horsepower compressors suitable for use in the system and method of the invention; DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to FIG. 1, refueling system 10 of the invention preferably comprises inlet source 12; compressor 14; intermediate storage tank 18; valves 22, 24, 26, 30, 32; check valves 34, 36 and flow lines 38, 40, 42, 44, 46. Refueling system 10 is preferably intended for use in refueling vehicle storage tank 16 with compressed natural gas. Although intermediate storage tank 18 and vehicle storage tank 16 are shown in FIG. 1 as single tanks, it will be appreciated by those of ordinary skill in the art upon reading this disclosure that a plurality of interconnected tanks can be substituted for either within the scope of the invention. Inlet source 12 preferably provides natural gas to refueling system 10 at a pressure ranging from about 330 up to about 1000 psig. As used herein, inlet source 12 can be a pipeline having an available line pressure of at least about 330 psig, or can be any other similarly effective source of gas at that pressure such as, for example, an auxiliary storage tank, a discharge line from a booster compressor, or the like. Means are preferably provided for selectively placing inlet source 12 in fluid communication with compressor 14 and/or with vehicle storage tank 16. Such means can include, for example, such flow lines, valves, gauges and meters as may be desirable to selectively control the flow of CNG between inlet source 12, compressor 14, vehicle storage tank 16, and intermediate storage tank 18 in accordance with the method of the invention. Although one preferred embodiment of the invention is disclosed in FIG. 1 and described in further detail below, it will be apparent to one of ordinary skill in the art upon reading this disclosure that other piping and valving arrangements can be similarly utilized without departing from the claimed invention. Where particular types of valves are shown, described, or otherwise referred to herein, it will likewise be understood that other types of valves can be similarly utilized within the scope of the invention. Thus, for example, electrically or pneumatically operated valves may be substituted for manually operated valves, manually operated valves may be substituted for check valves, and the like. Valves and other controllers not shown in FIG. 1 can also be added if desired to further control flow between individual vehicle storage tanks, intermediate storage tanks, or the like. Temperature and pressure gauges can be utilized as desired, and the entire system can be installed so as to be computer controlled or otherwise automated in response to measured temperatures, pressures, flow rates or the like throughout the system. According to a preferred embodiment of the invention, FIG. 1 discloses one inlet source 12 that communicates through flow line 38 with vehicle storage tank 16. Because FIG. 1 is a simplified block flow diagram, the mechanical interconnection between flow line 38 and vehicle storage tank 16 is not shown. In an actual installation of refueling system 10, the mechanical interconnection between flow line 38 of the refueling system and the vehicle being refueled could be a threaded connection situated, for example, between valve 24 and vehicle storage tank 16, or any other similarly effective interconnecting means. Although only one vehicle storage tank 16 is shown in FIG. 1, more tanks can be similarly utilized, depending upon factors such as tank size, vehicle configuration, the desired range of travel, and the like. Valve 22 preferably controls the flow of pressurized natural gas into refueling system 10 from inlet source 12. Check valves 34, 36 desirably control the direction of flow through line 38 toward vehicle storage tank 16 and prevent undesirable flow reversals that might otherwise occur due to unexpected pressure changes, leaks, equipment failures, or the like. Valve 24 controls the flow of pressurized natural gas into vehicle storage tank 16. Compressor 14 is preferably located and connected in such manner that line 38 communicates with compressor inlet line 40 downstream of check valve 34 and upstream of check valve 36. Compressor 14 is desirably a single stage hydraulic compressor designed and constructed so as to operate at suction pressures ranging from about 330 up to about 3600 psig and at discharge pressures ranging from about 330 psig up to about 4500 psig. Such compressors are commercially available, for example, from Hydro Pac, Inc. of Fairview, Pennsylvania. Commercially available vehicle storage tanks are typically rated at either 3000 or 3600 psig. Under the NGV-2 Standard established by the Natural Gas Vehicle Coalition, such tanks can be overfilled by 25% of their rated pressure. A 3000 psig rated tank could therefore be filled to 3750 psig and a 3600 psig rated tank could be filled to 4500 psig. For this reason, 4500 psig is said to be the preferred upper limit for the discharge pressure of compressor 14 utilized in the system and method of the invention. Compressors such as compressor 14 utilized in the present invention will generally be capable of compressing gasses such as natural gas at a ratio of about 8: 1, and ratios as high as about 10:1 may be achieved. FIG. 2 is a graph plotting suction pressure versus discharge rate (in cubic feet per minute) for CNG compressors operating at 20 and 40 horsepower with a discharge pressure of 3600 psig. Because of the wide range of acceptable suction pressures for such a compressor, it can be selectively supplied with natural gas either from inlet source 12 at a pressure as low as about 330 psig, or for reasons described in greater detail below in accordance with the method of the invention, ■ at intermediate storage pressures as high as about 3600 psig. Where CNG refueling system 10 of the invention is intended for use in a high volume application, such as, for example, in fleet refueling or in a commercial CNG refueling station, it is of course possible to connect two or more compressors 14 in parallel as required to provide a refueling capability during times when one of the compressors is shut down for maintenance or repair. Compressor discharge line 42 preferably communicates with flow line 38 downstream of check valve 36, and with at least one intermediate storage tank 18 through line 44. Gas flow through line 42 is preferably controlled by valve 26, disposed downstream from the connection between line 42 and line 44. Flow through line 44 is preferably controlled by valve 30. Line 46 preferably connects intermediate storage tank 18 through valve 32 with flow line 38 and with compressor inlet line 40 between check valves 34 and 36. The method of the invention is further described and explained in relation to the structural elements of refueling system 10 as described above. When refueling commences, vehicle storage tank 16 is first connected to flow line 38 downstream of valve 24. If the pressure in vehicle storage tank 16 is less than the available line pressure at inlet source 12 when refueling commences, valves 22, 24 are opened and gas is permitted to flow into tank 16 through flow line 38 until the pressure equalizes. If, during that time, the pressure in intermediate storage tank 18 is already at or above the preferred maximum intermediate storage pressure, valves 26, 30, 32 remain closed. If, on the other hand, the pressure in intermediate storage tank 18 is less than the preferred maximum intermediate storage pressure, compressor 14 is activated and valve 30 is opened, permitting CNG discharged from compressor 14 to flow into tank 18. If the pressure in storage tank 18 reaches the predetermined desired maximum level before the vehicle tank pressure equalizes with the inlet source pressure, compressor 14 will cease operation and valve 30 will desirably close. Although intermediate storage tank pressures ranging from about 330 psig to about 3600 psig can be experienced utilizing the present invention, the preferred maximum intermediate storage pressure is about 2700 psig because the greatest storage efficiency is achieved at intermediate storage pressures ranging from about 1700 psig to about 2700 psig (assuming a temperature of about 70°F), and most preferably, from about 2300 psig to about 2400 psig. If the pressure in vehicle storage tank 16 equalizes with the inlet source pressure before the pressure in intermediate storage tank 18 reaches the predetermined maximum level, or if the pressure in vehicle storage tank 16 is initially at a pressure greater than the inlet source pressure, vehicle storage tank 16 is preferably filled by simultaneously supplying CNG to tank 16 from compressor 14 and from intermediate storage tank 18 until such time as the pressure in vehicle storage tank 16 has equalized with the intermediate storage pressure. In this mode of operation, valves 22, 24, 26 and 30 are desirably open and valve 32 is closed, thereby permitting CNG to be supplied to vehicle storage tank 16 simultaneously from compressor 14 through lines 42, 38 and from intermediate storage tank 18 through lines 44, 42 and 38. CNG supplied to vehicle storage tank 16 from compressor 14 at this stage of refueling is compressed only to the prevailing vehicle storage tank pressure, and the rate of refueling is preferably accelerated by also supplying CNG to vehicle storage tank 16 from intermediate storage tank 18 at the intermediate storage pressure. The intermediate storage pressure when refueling begins is preferably within the range of from about 1700 to about 2700 psig, and most preferably within the range of from about 2300 to about 2400 psig, because the storage efficiencies for CNG at 70 °F are greatest within these pressure ranges. CNG supplied to vehicle storage tank 16 from intermediate storage tank 18 provides a maximum discharge volume per pound of pressure drop in the intermediate storage pressure because of the inherent efficiency in storing CNG at pressures between about 1700 and about 2700 psig at standard conditions. Less throughput and horsepower are required of compressor 14 than would otherwise be required to refill vehicle storage tank 16 because of the CNG being supplied from intermediate storage tank 18. Once the pressure in vehicle storage tank 16 has equalized with the pressure in intermediate storage tank 18 at a pressure that is below the intended full tank pressure of the vehicle, valve 30 is closed and valve 32 is opened. CNG is then preferably supplied to compressor 14 from intermediate storage tank 18 through valve 32 at a suction pressure equal to the prevailing intermediate storage pressure, and compressor 14 continues to discharge CNG into vehicle storage tank 16 through valves 26, 24 and lines 42, 38 until the desired full vehicle tank pressure is reached. By supplying CNG to the suction side of compressor 14 at an intermediate storage pressure preferably ranging from about 1700 to about 2700 psig, and most preferably, from about 2300 to about 2400 psig, rather than at the inlet source pressure, the compressor discharge rate (CFM) is significantly increased without increasing the necessary horsepower. The last step of the refueling method of the invention occurs when vehicle storage tank 16 is filled to the intended full tank pressure, and the compressor suction is switched back to the inlet source pressure by closing valve 32. At this time valves 24, 26 and 32 are closed and valves 22 and 30 are open. Compressor 14 desirably continues to operate until intermediate storage tank 18 is again returned to the preferred intermediate storage pressure in the range of from about 1700 to about 2700 psig, and most preferably, from about 2300 to about 2400 psig. With the vehicle refueling system and method disclosed herein, it is not necessary to complete vehicle storage tank refueling by compressing natural gas from the inlet source pressure to the maximum intended vehicle fill pressure; nor is it necessary to compress natural gas to intermediate storage pressures as high as the maximum intended vehicle fill pressure. The preferred pressures stated herein are based upon the compressibility of natural gas at about 70°F, and it will be appreciated by those of ordinary skill in the art that such pressures can vary if the ambient temperatures are substantially above or below standard conditions. It will similarly be appreciated that in describing the system and method of the invention as disclosed herein, intervening pressure drops through flow lines, valves, gauges, and the like are not addressed, but will generally be relatively insignificant due to the short line lengths within the system. Also, while the system and method of the invention are disclosed herein in relation to a preferred embodiment for compressing natural gas and for refueling vehicle storage tanks with natural gas, it will be appreciated that the subject system and method are similarly applicable to other gasses and uses. Other alterations and modifications of the invention will likewise become apparent to those of ordinary skill in the art upon reading the present disclosure, and it is intended that the scope of the invention disclosed herein be limited only by the broadest interpretation of the appended claims to which the inventor is legally entitled.

Claims: AMENDED CLAIMS [received by the International Bureau on 1 March 1995 (01.03.95); original claim 1 amended; remaining claims unchanged (1 page)] 1. A CNG refueling system for a motor vehicle, the system comprising: at least one vehicle storage tank for storing CNG at a maximum intended vehicle storage tank fill pressure ranging from about 3000 to about 4500 psig; at least one compressor operable over a range of suction pressures ranging from about 330 to about 3600 psig and a range of discharge pressures ranging from about 330 psig to about 4500 psig; at least one intermediate storage tank for storing CNG at pressures ranging from about 330 to about 3600 psig; means for selectively delivering natural gas received from an external source at a pressure less than about 1000 psig into the motor vehicle storage tank until the vehicle storage tank pressure equalizes with the pressure of the external source; means for selectively delivering natural gas received from the external source to the compressor and for delivering the CNG discharged from the compressor into the intermediate storage tank until the pressure in the intermediate storage tank reaches a predetermined maximum level not greater than about 3600 psig; means for selectively and simultaneously delivering CNG to the vehicle storage tank from the intermediate storage tank and from the compressor until the vehicle storage tank pressure equalizes with the intermediate storage tank pressure; means for supplying CNG to the compressor from the intermediate storage tank for further compression and means for discharging the further-compressed CNG into the vehicle storage tank until the vehicle storage tank pressure reaches the maximum intended vehicle storage fill pressure. STATEMENT UNDER ARTICLE 19 AMENDMENT Applicant hereby respectfully requests the entry of an Amendment to Claim 1 as shown on the attached Replacement Sheet Page 16, said Amendment being made as follows: 1. In Claim 1, line 5, delete "single stage". REMARKS In reviewing the corresponding U.S. Priority Application Serial No. 08/ 127, 426, filed September 27, 1993, prior to its issuance as U.S. 5,351,726 on October 4, 1994, Applicant noted that the recitation of a "single stage" compressor at claim 1, line 5 was not required by the disclosure and was not required to patentably distinguish the claimed invention over the cited prior art. Applicant then requested and was granted an amendment deleting the recitation "single stage" from claim 1 of U.S. 5,351,726. While the apparatus of the invention requires a "compressor" (e.g., at page 10, lines 3, 17 and 20) as one element of the subject CNG refueling system, the use of a "single stage" compressor is merely disclosed (e.g., at page 11, line 26) as being desirable. The possible use of a "booster compressor" as an additional stage is discussed at page 10, lines 15-16. The amendment of claim 1 to delete the recitation "single stage" prior to substantive examination is therefore respectfully requested. The recitation of a "single stage" compressor still appears in claims 5 and 6.

Inventors: DIGGINS DAVID ANDREW, DIGGINS, DAVID, ANDREW
Applicants: WAGNER & BROWN LTD, WAGNER & BROWN, LTD.
Application year: 1994
Main classification: B65B31
IPC codes: F17C5